WO1998001414A1 - Verfahren zur reinigung von roh-acrylsäure durch kristallisation - Google Patents
Verfahren zur reinigung von roh-acrylsäure durch kristallisation Download PDFInfo
- Publication number
- WO1998001414A1 WO1998001414A1 PCT/EP1997/003304 EP9703304W WO9801414A1 WO 1998001414 A1 WO1998001414 A1 WO 1998001414A1 EP 9703304 W EP9703304 W EP 9703304W WO 9801414 A1 WO9801414 A1 WO 9801414A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- acrylic acid
- weight
- acid
- crystallization
- crude
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C57/00—Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms
- C07C57/02—Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms with only carbon-to-carbon double bonds as unsaturation
- C07C57/03—Monocarboxylic acids
- C07C57/04—Acrylic acid; Methacrylic acid
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
Definitions
- the present invention relates to a process for the purification of crude acrylic acid by crystallization.
- Acrylic acid either alone or in the form of its salts or its esters, is particularly important for the preparation of polymers for a wide variety of applications (for example adhesives, superabsorbents, binders).
- acrylic acid can be obtained by catalytic gas phase oxidation of propane, propene and / or acrolein. These starting gases, usually diluted with inert gases such as nitrogen, CO 2 and / or water vapor, are passed in a mixture with oxygen at elevated temperatures and, if appropriate, increased pressure, over transition-metal mixed oxide catalysts and oxidatively converted into a product mixture containing acrylic acid. Condensation of the product mixture or by absorption in a suitable absorbent (e.g. water or a mixture of 70 to 75% by weight of diphenyl ether and 25 to 30% by weight of diphenyl) can result in a basic separation of the acrylic acid from the product gas flow ( see e.g. EP-A 297 445 and DE-PS 21 36 396).
- a suitable absorbent e.g. water or a mixture of 70 to 75% by weight of diphenyl ether and 25 to 30% by weight of diphenyl
- an acrylic acid is often obtained, which is referred to here as crude acrylic acid.
- This raw acrylic acid is not a pure product. Rather, it contains a spectrum of different impurities typical of the gas-phase catalytically oxidative production route. These are in particular acetic acid, propionic acid, water and low molecular weight aldehydes such as acrolein, methacrolein, propionaldehyde, n-butyraldehyde, benzaldehyde, furfural and crotonaldehyde.
- Another typical component of crude acrylic acid is polymerization inhibitors.
- Dibenzo- 1,4-thiazine is a colorless one, at 180 ° C
- dibenzo- 1, 4 -thiazine is usually used either as the sole acrylic acid process stabilizer or in combination with other possible acrylic acid process stabilizers such as.
- diacrylic acid is a slow process. If you leave a purity of> .99.5% by weight of acrylic acid at 25 ° C, 1 bar, the formation of diacrylic acid is about 150 ppm per day, based on the weight of acrylic acid. The total amount of other secondary components possibly contained in the crude acrylic acid, based on the weight of the crude acrylic acid, is generally not more than 10% by weight.
- crude acrylic acid is to be understood as meaning acrylic acid which, if its content of acrylic acid oligomers 2) (Michael adducts) is disregarded,
- the data in% by weight are based on the weight of the crude acrylic acid minus its content of acrylic acid oligomers.
- crude acrylic acid is to be understood as meaning acrylic acid which, if its content of acrylic acid oligomers is disregarded,
- crude acrylic acid used here thus also includes those acrylic acid which, if their content of acrylic acid oligomers is disregarded,
- acrylic acid ohgomers always mean the corresponding Michael adducts and acrylic acid oggomers not formed by radical polymerization, since the formation of the latter is essentially suppressed by the presence of polymerization inhibitors > 90% by weight acrylic acid, ⁇ . 5% by weight of acetic acid,
- the corresponding acetic and propionic acid esters would also be formed in side reactions, which reduces the yield of the desired acrylic acid ester, based on the amount of alkanol used .
- the acrylic acid esters formed in the presence of the low molecular weight aldehydes are used in radical polymerizations, their content of the low molecular weight aldehydes usually has an effect, for example, B. disadvantageous in that it z. B. the induction time of polymerization reactions, d. H. , influence the period between reaching the polymerization temperature and the actual start of the polymerization. Furthermore, they generally influence the degree of polymerization and can also cause discoloration in the polymers.
- esterification-compatible acrylic acid with a degree of purity of at least 98% by weight, based on the sum of all components, often even with a degree of purity of> 99% by weight.
- Pure acrylic acid is therefore normally produced by directly processing freshly prepared crude acrylic acid, since it contains practically no acrylic acid oligomers formed. Pure acrylic acid produced is usually consumed fresh.
- fractional crystallization is expediently used as the cleaning method, as is the case, for. B. is described in EP-A 616 998, since the fractional crystallization at low temperatures (according to Louis F. Fieser and Mary Fieser, Organic Chemistry, Verlag Chemie (1975), p. 422, Table 11.1.) Is Melting point of pure acrylic acid at 1 bar 13 ° C; the presence of foreign components lowers this position of the crystallization temperature) and low temperatures additionally inhibit both Michael addition and the radical polymerization of acrylic acid.
- a disadvantage of the purification of crude acrylic acid by crystallization is, however, the low solubility of dibenzo-1,4-thiazine in acrylic acid, which is about 1.5% by weight at 25 ° C. and only about 0.9 at 15 ° C. % By weight, based on the solution consisting of acrylic acid and dibenzo-1,4-thiazine.
- the presence of acetic acid and / or propionic acid in acrylic acid hardly influences these solubility values, whereas the presence of water still reduces the solubility of dibenzo-1,4-thiazine. The main consequence of this is as follows.
- acrylic acid is accompanied by an enrichment of the dibenzo -1,4 -thiazine in the remaining melt until the eutectic composition is reached and no longer pure acrylic acid separates but the eutectic mixture of dibenzo-1,4-thiazine and acrylic acid.
- the object of the present invention was therefore to increase the solubility of di-benzo-1,4-thiazine in acrylic acid by means of a suitable measure, thereby increasing the proportion of dibenzo-1,4-thiazine in the corresponding eutectic mixture and thus a to provide an improved process for the purification of crude acrylic acid by crystallization.
- the solubility of dibenzo-1,4-thiazine in acrylic acid can be increased by more than 100%, especially at the temperatures relevant to crystallization.
- a process for the purification of crude acrylic acid by crystallization which is characterized in that the diacrylic acid content of the crude acrylic acid before the crystallization step is at least 1% by weight, based on the weight the raw acrylic acid.
- Processes according to the invention are accordingly processes for the purification of crude acrylic acid, the content of diacrylic acid prior to the crystallization step of 1 to 2% by weight, or 1 to 3% by weight, or 1 to 5% by weight. %, or 1 to 10% by weight, or 1 to 20% by weight, or 1 to 40% by weight.
- a diacrylic acid content of the crude acrylic acid which is to be crystallisatively purified is generally not more than 50% by weight.
- the process according to the invention is therefore applicable to crude acrylic acid, the content of dibenzo-1,4-thiazine based on the weight of the crude acrylic acid minus the amount of acrylic acid oligomers contained therein. 0.9% by weight, or> . 1% by weight, or> 1, 1% by weight, or> 1, 2 Ge. -%, or> 1.3% by weight, or> 1.4% by weight, or> 1.5% by weight.
- the content of dibenzo-1,4-thiazine obtained in this way will not be more than 2% by weight.
- the process according to the invention can also be used if the crude acrylic acid contains up to 5% by weight of hydroquinone.
- diacrylic acid itself has an increased solubility in acrylic acid. It is also advantageous that diacrylic acid can be split back into acrylic acid using an elevated temperature.
- the adjustment according to the invention of the diacrylic acid content of the crude acrylic acid to be crystallisatively cleaned can be achieved in different ways.
- the crude acrylic acid to be cleaned can contain a small amount of a strong protic mineral acid such as. B. H 2 S0, HC1 or H 3 P0 can be added, which catalyzes the Michael addition of acrylic acid.
- the presence of H 2 0 also favors diacrylic acid formation.
- the catalytic effect of the mineral acid can be neutralized by adding a neutralizing base.
- the diacrylic acid content can also be increased by adding some of the rest in the first separation steps separates contained components, z. B. by distillation and / or crystallization.
- diacrylic acid can also be grown in pure acrylic acid, e.g. B. by distillation and add the crude acrylic acid to be purified crystallisatively.
- the process according to the invention is normally carried out at normal pressure, ie. H. , carried out at a pressure of 1 bar.
- the method according to the invention is usually implemented as fractional crystallization.
- the individual crystallization stages can be implemented both as static and / or as dynamic crystallization.
- Layer crystallization such as falling film crystallization as well as suspension crystallization can be used. A detailed description of these crystallization modes can be found in EP-A 616 998 and in the literature cited therein.
- acrylic acid suitable for esterification is initially continuously produced. Since it must be process stabilized in the course of the esterification, dibenzo-1,4-thiazine still contained therein does not have a disadvantageous effect (for esterification-compatible acrylic acid, the upper limit of the dibenzo-1,4-thiazine content to be observed is 750 ppm (on the Based on weight) and the corresponding limit for diacrylic acid is 1.5% by weight; for pure acrylic acid the upper limit of the dibenzo -1,4 -thiazine content to be observed is 1 ppm and the corresponding limit for diacrylic acid is 0.2% by weight. -% in the case of use for conventional polymerizations and at 500 ppm in the case of use for the production of superabsorbers;).
- the acrylic acid produced, suitable for esterification and containing dibenzo-1,4-thiazine, is then at least partially stored, whereby this temporary storage can last a few days, a week, a month, a quarter, a half year or longer.
- Acrylic acid contained in this intermediate storage can then be used for the production of acrylic acid esters or for the crystallizative production of pure acrylic acid, as required.
- the formation of diacrylic acid which occurs in the meantime during the storage and which is usually attempted to be prevented in the course of the production of pure acrylic acid has only a limited disadvantageous effect in the esterification, since via a cleavage ultimately involved in the processing of the esterification mixture, based on the alkanol used, Loss of yield can be prevented.
- the diacrylic acid formed in the course of storage has an advantageous effect on the further purification of esterified acrylic acid to produce pure acrylic acid which is essentially free of dibenzo-1-thiazine.
- Table 1 shows the increase in solubility of dibenzo-1,4-thiazine in acrylic acid associated with increasing diacrylic acid content for two temperatures used as a result of solubility tests.
- Table 2 shows the solubility of di-benzo-1, - thiazine in acetic acid.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Nitrogen- Or Sulfur-Containing Heterocyclic Ring Compounds With Rings Of Six Or More Members (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
MX9809574A MX203355B (es) | 1996-07-10 | 1997-06-24 | Purificacion de acido acrilico crudo por cristalizacion |
AU33440/97A AU3344097A (en) | 1996-07-10 | 1997-06-24 | Process for purifying crude acrylic acid by crystallization |
EP97929277A EP0912486B1 (de) | 1996-07-10 | 1997-06-24 | Verfahren zur reinigung von roh-acrylsäure durch kristallisation |
JP10504708A JP2000514069A (ja) | 1996-07-10 | 1997-06-24 | 結晶化による粗製アクリル酸の精製法 |
BR9710217A BR9710217A (pt) | 1996-07-10 | 1997-06-24 | Processo para purificar por cristalização em ácido acrilico bruto |
DE59702539T DE59702539D1 (de) | 1996-07-10 | 1997-06-24 | Verfahren zur reinigung von roh-acrylsäure durch kristallisation |
US09/147,457 US6063959A (en) | 1996-07-10 | 1997-06-24 | Purification of crude acrylic acid by crystallization |
KR19997000138A KR100502603B1 (ko) | 1996-07-10 | 1997-06-24 | 결정화에 의한 조 아크릴산의 정제 방법 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19627679.9 | 1996-07-10 | ||
DE19627679A DE19627679A1 (de) | 1996-07-10 | 1996-07-10 | Verfahren zur Reinigung von Roh-Acrylsäure durch Kristallisation |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998001414A1 true WO1998001414A1 (de) | 1998-01-15 |
Family
ID=7799366
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1997/003304 WO1998001414A1 (de) | 1996-07-10 | 1997-06-24 | Verfahren zur reinigung von roh-acrylsäure durch kristallisation |
Country Status (15)
Country | Link |
---|---|
US (1) | US6063959A (de) |
EP (1) | EP0912486B1 (de) |
JP (1) | JP2000514069A (de) |
KR (1) | KR100502603B1 (de) |
CN (1) | CN1072203C (de) |
AU (1) | AU3344097A (de) |
BR (1) | BR9710217A (de) |
CA (1) | CA2250806A1 (de) |
CZ (1) | CZ5099A3 (de) |
DE (2) | DE19627679A1 (de) |
ID (1) | ID17665A (de) |
MX (1) | MX203355B (de) |
MY (1) | MY116928A (de) |
TW (1) | TW427972B (de) |
WO (1) | WO1998001414A1 (de) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007043748A1 (de) | 2007-09-13 | 2008-09-11 | Basf Se | Verfahren zur kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
DE102007043759A1 (de) | 2007-09-13 | 2008-09-11 | Basf Se | Verfahren zum Betreiben einer kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
DE102007043758A1 (de) | 2007-09-13 | 2008-10-23 | Basf Se | Verfahren zum Betreiben einer kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat des Zielproduktes X |
DE102008040799A1 (de) | 2008-07-28 | 2008-12-11 | Basf Se | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enthaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal |
DE102008042008A1 (de) | 2007-09-13 | 2009-04-09 | Basf Se | Verfahren zur kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
DE102008041573A1 (de) | 2008-08-26 | 2010-03-04 | Basf Se | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enhaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal |
DE102010042216A1 (de) | 2010-10-08 | 2011-06-09 | Basf Se | Verfahren zur Hemmung der unerwünschten radikalischen Polymerisation von in einer flüssigen Phase P befindlicher Acrylsäure |
US8299299B2 (en) | 2008-07-28 | 2012-10-30 | Basf Se | Process for separating acrylic acid present as a main constituent and glyoxal present as a by-product in a product gas mixture of a partial heterogeneously catalyzed gas phase oxidation of a C3 precursor compound of acrylic acid |
CZ303896B6 (cs) * | 2000-04-11 | 2013-06-12 | Basf Aktiengesellschaft | Zpusob cistení taveniny surové kyseliny akrylové |
US9763801B2 (en) | 2007-09-13 | 2017-09-19 | Globus Medical, Inc. | Transcorporeal spinal decompression and repair systems and related methods |
WO2020020697A1 (de) | 2018-07-26 | 2020-01-30 | Basf Se | Verfahren zur hemmung der unerwünschten radikalischen polymerisation von in einer flüssigen phase p befindlicher acrylsäure |
WO2021191042A1 (de) | 2020-03-26 | 2021-09-30 | Basf Se | Verfahren zur hemmung der unerwünschten radikalischen polymerisation von in einer flüssigen phase p befindlicher acrylsäure |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19904820A1 (de) * | 1999-02-05 | 2000-08-10 | Stockhausen Chem Fab Gmbh | Verfahren und Vorrichtung zur Reinigung von Stoffen mittels Kristallisation |
DE10003498A1 (de) * | 2000-01-27 | 2001-08-02 | Basf Ag | Reinigungsverfahren für (Meth)acrylsäure |
DE10122788A1 (de) * | 2001-05-10 | 2002-06-06 | Basf Ag | Verfahren der kristallisativen Reinigung einer Roh-Schmelze wenigstens eines Monomeren |
DE10257449A1 (de) * | 2002-12-09 | 2003-11-06 | Basf Ag | Verfahren zur Herstellung geruchsarmer Hydrogel-bildender Polymerisate |
DE10347664A1 (de) | 2003-10-09 | 2004-12-02 | Basf Ag | Verfahren der rektifikativen Auftrennung einer Acrylsäure enthaltenden Flüssigkeit |
JP2005247731A (ja) * | 2004-03-03 | 2005-09-15 | Mitsubishi Chemicals Corp | (メタ)アクリル酸組成物及びその製造方法 |
US7601866B2 (en) | 2005-03-01 | 2009-10-13 | Basf Aktiengesellschaft | Process for removing methacrolein from liquid phase comprising acrylic acid as a main constituent and target product, and methacrolein as a secondary component |
US7705181B2 (en) * | 2005-03-01 | 2010-04-27 | Basf Akiengesellschaft | Process for removing methacrylic acid from liquid phase comprising acrylic acid as a main constituent and target product, and methacrylic acid as a secondary component |
US8292863B2 (en) | 2009-10-21 | 2012-10-23 | Donoho Christopher D | Disposable diaper with pouches |
DE102012201913A1 (de) * | 2012-02-09 | 2013-08-14 | Tesa Se | Haftklebebänder auf Basis biobasierter Monomere |
EP3012244A1 (de) | 2014-10-24 | 2016-04-27 | Sulzer Chemtech AG | Verfahren und Vorrichtung zur Reinigung von Acrylsäure |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE786398A (fr) * | 1971-07-21 | 1973-01-18 | Basf Ag | Procede de preparation de l'acide acrylique anhydre |
DE3721865A1 (de) * | 1987-07-02 | 1989-01-12 | Basf Ag | Verfahren zur herstellung von methacrylsaeure |
TW305830B (de) * | 1993-03-26 | 1997-05-21 | Sulzer Chemtech Ag | |
DE4335172A1 (de) * | 1993-10-15 | 1995-04-20 | Basf Ag | Verfahren zur Reinigung von Roh-(Meth)acrylsäure |
-
1996
- 1996-07-10 DE DE19627679A patent/DE19627679A1/de not_active Withdrawn
-
1997
- 1997-06-24 JP JP10504708A patent/JP2000514069A/ja not_active Ceased
- 1997-06-24 BR BR9710217A patent/BR9710217A/pt not_active IP Right Cessation
- 1997-06-24 CZ CZ9950A patent/CZ5099A3/cs unknown
- 1997-06-24 US US09/147,457 patent/US6063959A/en not_active Expired - Fee Related
- 1997-06-24 CA CA002250806A patent/CA2250806A1/en not_active Abandoned
- 1997-06-24 AU AU33440/97A patent/AU3344097A/en not_active Abandoned
- 1997-06-24 EP EP97929277A patent/EP0912486B1/de not_active Expired - Lifetime
- 1997-06-24 WO PCT/EP1997/003304 patent/WO1998001414A1/de not_active Application Discontinuation
- 1997-06-24 CN CN97194221A patent/CN1072203C/zh not_active Expired - Fee Related
- 1997-06-24 KR KR19997000138A patent/KR100502603B1/ko not_active IP Right Cessation
- 1997-06-24 MX MX9809574A patent/MX203355B/es not_active IP Right Cessation
- 1997-06-24 DE DE59702539T patent/DE59702539D1/de not_active Expired - Fee Related
- 1997-07-10 ID IDP972392A patent/ID17665A/id unknown
- 1997-07-10 TW TW086109744A patent/TW427972B/zh not_active IP Right Cessation
- 1997-07-10 MY MYPI97003134A patent/MY116928A/en unknown
Non-Patent Citations (1)
Title |
---|
No relevant documents disclosed * |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CZ303896B6 (cs) * | 2000-04-11 | 2013-06-12 | Basf Aktiengesellschaft | Zpusob cistení taveniny surové kyseliny akrylové |
DE102007043759A1 (de) | 2007-09-13 | 2008-09-11 | Basf Se | Verfahren zum Betreiben einer kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
DE102007043758A1 (de) | 2007-09-13 | 2008-10-23 | Basf Se | Verfahren zum Betreiben einer kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat des Zielproduktes X |
DE102008042008A1 (de) | 2007-09-13 | 2009-04-09 | Basf Se | Verfahren zur kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
DE102008042009A1 (de) | 2007-09-13 | 2009-04-09 | Basf Se | Verfahren zum Betreiben einer kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat des Zielproduktes X |
DE102008042010A1 (de) | 2007-09-13 | 2009-04-16 | Basf Se | Verfahren zum Betreiben einer kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
DE102007043748A1 (de) | 2007-09-13 | 2008-09-11 | Basf Se | Verfahren zur kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
US9763801B2 (en) | 2007-09-13 | 2017-09-19 | Globus Medical, Inc. | Transcorporeal spinal decompression and repair systems and related methods |
DE102008040799A1 (de) | 2008-07-28 | 2008-12-11 | Basf Se | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enthaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal |
US8299299B2 (en) | 2008-07-28 | 2012-10-30 | Basf Se | Process for separating acrylic acid present as a main constituent and glyoxal present as a by-product in a product gas mixture of a partial heterogeneously catalyzed gas phase oxidation of a C3 precursor compound of acrylic acid |
DE102008041573A1 (de) | 2008-08-26 | 2010-03-04 | Basf Se | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enhaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal |
DE102010042216A1 (de) | 2010-10-08 | 2011-06-09 | Basf Se | Verfahren zur Hemmung der unerwünschten radikalischen Polymerisation von in einer flüssigen Phase P befindlicher Acrylsäure |
US9212122B2 (en) | 2010-10-08 | 2015-12-15 | Basf Se | Process for inhibiting unwanted free-radical polymerization of acrylic acid present in a liquid phase P |
WO2012045738A1 (de) | 2010-10-08 | 2012-04-12 | Basf Se | Verfahren zur hemmung der unerwünschten radikalischen polymerisation von in einer flüssigen phase p befindlicher acrylsäure |
WO2020020697A1 (de) | 2018-07-26 | 2020-01-30 | Basf Se | Verfahren zur hemmung der unerwünschten radikalischen polymerisation von in einer flüssigen phase p befindlicher acrylsäure |
US11447439B2 (en) | 2018-07-26 | 2022-09-20 | Basf Se | Method for inhibiting unwanted radical polymerisation of acrylic acid present in a liquid phase P |
WO2021191042A1 (de) | 2020-03-26 | 2021-09-30 | Basf Se | Verfahren zur hemmung der unerwünschten radikalischen polymerisation von in einer flüssigen phase p befindlicher acrylsäure |
Also Published As
Publication number | Publication date |
---|---|
CZ5099A3 (cs) | 1999-05-12 |
MX203355B (es) | 2001-07-30 |
CN1072203C (zh) | 2001-10-03 |
MX9809574A (es) | 1999-03-31 |
BR9710217A (pt) | 1999-08-10 |
ID17665A (id) | 1998-01-15 |
MY116928A (en) | 2004-04-30 |
DE19627679A1 (de) | 1998-01-15 |
JP2000514069A (ja) | 2000-10-24 |
DE59702539D1 (de) | 2000-11-30 |
US6063959A (en) | 2000-05-16 |
KR20000023681A (ko) | 2000-04-25 |
KR100502603B1 (ko) | 2005-07-21 |
TW427972B (en) | 2001-04-01 |
EP0912486B1 (de) | 2000-10-25 |
CN1216975A (zh) | 1999-05-19 |
AU3344097A (en) | 1998-02-02 |
CA2250806A1 (en) | 1998-01-15 |
EP0912486A1 (de) | 1999-05-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0912486B1 (de) | Verfahren zur reinigung von roh-acrylsäure durch kristallisation | |
DE2804449C2 (de) | Verfahren zum Inhibieren der Polymerisation einer leicht polymerisierbaren aromatischen Vinylverbindung | |
DD282909A5 (de) | Verfahren zur gewinnung von reinem dimethylether (dme) | |
DE2164767A1 (de) | ||
DE2121123C3 (de) | Verfahren zum Abtrennen von Wasser aus wäßrigen Lösungen von Acrylsäure durch azeotrope Destillation | |
DE102008040799A1 (de) | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enthaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal | |
EP2334631B1 (de) | Verfahren zur auftrennung von in einem produktgasgemisch einer partiellen heterogen katalysierten gasphasenoxidation einer c3-vorläuferverbinding der acrylsäure als hauptbestandteil enthaltener acrylsäure und als nebenprodukt enthaltenem glyoxal | |
DE102008041573A1 (de) | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enhaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal | |
EP0713854B1 (de) | Verfahren zur Reinigung von Roh-(Meth)acrylsäure | |
DE69111382T2 (de) | Polymerisationsinhibitor und Inhibierungsmethode für Vinylverbindungen. | |
DE2144920C3 (de) | Verfahren zur Herstellung von p-Toluylsäure und Monomethylterephthalat | |
DE69114486T2 (de) | Verfahren zur Reinigung von Glycidyl(meth)acrylat. | |
EP1286943B1 (de) | Verfahren der diskontinuierlichen kristallisativen reinigung von roh-acrylsäure | |
DE3874667T2 (de) | Verfahren zur reinigung von methacrylsaeure. | |
DE19923389A1 (de) | Verfahren zum Lagern und/oder Transportieren von Reinacrylsäure | |
WO2010105894A2 (de) | Für eine aufreinigung stabilisierte zusammensetzung und verfahren zur aufreinigung und zur herstellung von hydroxyalkyl(meth)acrylaten | |
EP0080023B1 (de) | Verfahren zum kontinuierlichen Verestern von Methacrylsäure | |
EP1856021B1 (de) | Verfahren zur abtrennung von methacrolein aus acrylsäure als hauptbestandteil sowie zielprodukt und methacrolein als nebenkomponente enthaltender flüssiger phase | |
EP1057805A1 (de) | Verfahren zur Herstellung von Isobornylmethacrylat | |
DE3009946C2 (de) | Verfahren zur Gewinnung von Methacrylsäure | |
AT404592B (de) | Verfahren zur herstellung von wässrigen o-phthalaldehyd-glutaraldehydlösungen | |
EP1856020B1 (de) | Verfahren zur abtrennung von methacrylsäure aus acrylsäure als hauptbestandteil sowie zielprodukt und methacrylsäure als nebenkomponente enthaltender flüssiger phase | |
WO2020020697A1 (de) | Verfahren zur hemmung der unerwünschten radikalischen polymerisation von in einer flüssigen phase p befindlicher acrylsäure | |
DE2715293C2 (de) | ||
EP0581222B1 (de) | Verfahren zur Abtrennung von Methacrolein aus einem gasförmigen Gemisch |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 97194221.8 Country of ref document: CN |
|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AL AU BG BR CA CN CZ GE HU IL JP KR LT LV MX NO NZ PL RO SG SI SK TR UA US AM AZ BY KG KZ MD RU TJ TM |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1997929277 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2250806 Country of ref document: CA Ref document number: 2250806 Country of ref document: CA Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: PA/a/1998/009574 Country of ref document: MX |
|
WWE | Wipo information: entry into national phase |
Ref document number: 09147457 Country of ref document: US |
|
WWE | Wipo information: entry into national phase |
Ref document number: PV1999-50 Country of ref document: CZ |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1019997000138 Country of ref document: KR |
|
WWP | Wipo information: published in national office |
Ref document number: 1997929277 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: PV1999-50 Country of ref document: CZ |
|
WWP | Wipo information: published in national office |
Ref document number: 1019997000138 Country of ref document: KR |
|
WWG | Wipo information: grant in national office |
Ref document number: 1997929277 Country of ref document: EP |
|
WWG | Wipo information: grant in national office |
Ref document number: 1019997000138 Country of ref document: KR |
|
WWR | Wipo information: refused in national office |
Ref document number: PV1999-50 Country of ref document: CZ |